Co-initiated polyether polyol and process for its preparation

Abstract

Process for the preparation of a co-initiated polyether polyol, which process comprises the steps of (a) preparing a mixture of at least one aromatic initiator, at least one polyethylene glycol and optionally one or more aliphatic initiators, (b) reacting the mixture obtained in step (a) in the presence of a suitable alkoxylation catalyst with at least one alkylene oxide having three or more carbon atoms per molecule using such quantity of alkylene oxide that the polyether polyol obtained has a hydroxyl value in the range of from 150 to 400 mg KOH/g, and (c) recovering the co-initiated polyether polyol. The co-initiated polyether polyol is very suitable for (the preparation of rigid polyisocyanurate-modified polyurethane foams. Such foams have a good flame retardancy.

1 . Process for the preparation of a co-initiated polyether polyol, which process comprises the steps of: 
 (a) preparing a mixture of: 
 (a1) at least one aromatic initiator containing at least two active hydrogen atoms per molecule and  
 (a2) at least one polyethylene glycol having a molecular weight in the range of from 400 to 1000 and  
 (a3) optionally one or more aliphatic initiators containing from 2 to 6 active hydrogen atoms per molecule in an amount of at most 20 mole % based on total moles of (a1) and (a3), wherein the molar ratio of (a1) to (a2) is in the range of from 0.5:1 to 5:1,  
   (b) reacting the mixture obtained in step (a) in the presence of a suitable alkoxylation catalyst with at least one alkylene oxide having three or more carbon atoms per molecule using such quantity of alkylene oxide that the polyether polyol obtained has a hydroxyl value in the range of from 150 to 400 mg KOH/g, and    (c) recovering the co-initiated polyether polyol.    
     
     
         2 . Process according to  claim 1 , wherein one aromatic initiator is mixed with one polyethylene glycol in step (a) in a molar ratio of aromatic initiator (a1) to polyethylene glycol (a2) of from 1:1 to 4:1.  
     
     
         3 . Process according to  claim 2 , wherein the aromatic initiator is bisphenol A.  
     
     
         4 . Process according to any one of claims  1 - 3 , wherein such quantity of alkylene oxide is used in step (b) that the polyether polyol obtained has a hydroxyl value in the range of from 200 to 300.  
     
     
         5 . Process according to any one of claims  1 - 4 , wherein the sole alkylene oxide used in step (b) is propylene oxide.  
     
     
         6 . Co-initiated polyether polyol having an aromaticity in the range of from 5 to 35 wt % and an average molecular weight in the range of from 300 to 1000, which polyether polyol is obtainable by a process as claimed in any one of claims  1 - 5 .  
     
     
         7 . Co-initiated polyether polyol according to  claim 6  having an ethylene oxide content in the range of from 20 to 60 wt %, preferably 30 to 50 wt %.  
     
     
         8 . Polyether polyol formulation comprising a co-initiated polyether polyol as claimed in  claim 6  or  7  in admixture with a rigid, aromatic polyether polyol having a hydroxyl value of at least 400 mg KOH/g, preferably of from 500 to 600, and an average nominal functionality of at least 3.  
     
     
         9 . Process for the preparation of a rigid polyisocyanurate-containing polyurethane foam, which process comprises foaming a formulation comprising 
 (a) a co-initiated polyether polyol as claimed in  claim 6  or  7  or a polyether polyol formulation as claimed in  claim 8 ,    (b) a polyisocyanate in such amount that the isocyanate index is at least 150, preferably from 180 to 600,    (c) polyurethane catalyst and/or polyisocyanurate catalyst,    (d) one or more blowing agents, and    (e) usual auxiliaries.    
     
     
         10 . Rigid polyisocyanurate-containing polyurethane foam obtainable by the process according to  claim 9.